Process of emitting of hydrogen peroxide vapor

ABSTRACT

Method of emitting peroxide vapors or mixtures thereof, where the hydrogen peroxide is placed into a vessel, whereupon an initiator, catalyst or their precursor—ferrocene is added, from which the initiator or catalyst is created by reaction with peroxide or peroxide mixture.

TECHNICAL FIELD

The invention relates to generation of vapors for the need of decontamination by gaseous media.

STATE OF THE ART

Various medias are currently used for the need of gaseous decontamination for decontamination purposes: chlorine dioxide, hydrogen peroxide, formaldehyde, oxirane, methylbromide and others. Some medias are used directly in the gaseous state—methyl, bromide, oxirane, some are generated directly before use—chlorine dioxide, further various methods of evaporating are being used for longer period of time—hydrogen peroxide, formaldehyde.

There is a wide range of apparatus used for evaporation. Such devices are known, for example, from documents WO2007/008205, US2005/0074359 or US2005/0084415. However, there is always a large number of parts and complicated manipulation common to these solutions where both require connection to the media as power, compressed air, etc., and the vapor emission is single for one performance.

The aim of present invention is to provide a method of emitting hydrogen peroxide which would be simple, efficient, without need of any energy connection, and which would be able to replace the other used methods of gaseous decontamination.

SUMMARY OF THE INVENTION

The aforementioned drawbacks are largely eliminated by the method of hydrogen peroxide vapor emitting according to the invention, whose principle lies in placing hydrogen peroxide into a vessel, whereupon an initiator, catalyst or their precursor—ferrocene is added, from which the initiator or catalyst is created by reaction with peroxide or peroxide mixture.

In a preferred embodiment is the initiator, catalyst or the precursor selected from the group of metals such as silver, gold, platinum, palladium; metal oxides such as manganese, silver, aluminum, iron; Metal salts such as manganese, aluminum, iron, silver; Organometallics, manganese, iron, aluminum—e.g. ferrocen or metal-containing mixtures such as iron, aluminum, manganese, silver or their compounds.

In another preferred embodiment the peroxide is used in the range of concentration between 10-90% and the temperature of usability of given configuration is from −10 to 100° C.

In another preferred embodiment for long-term exposure by decontaminating vapors, the process is repeated with a new charge of peroxide, or mixture and by adding of a new source of initiator or catalyst.

In another preferred embodiment the peroxide mixture is a peroxide mixed with one or more substances such as peroxyacetic acid, peroxyformate acid, formic acid, boric acid, phosphoric acid, organic or inorganic carbonates, N oxides, alcohols such as tert-butyl alcohol, amines, esters; monosylic, dibasic or tribasic carboxylic acids such as oxalic acid, acetic acid, citric acid, malic acid, tartaric acid, complexing agents such as chelatones, Komlexon I, II, III, the transition metal salts catalyzing the Fenton reaction, such as salts of iron, copper, silver, manganese and zinc.

In another preferred embodiment the emissions of the vapors is carried out directly in the treated space, or the vapors are brought through the pipeline route to the required destination.

In another preferred embodiment the gases or vapors emitted are diluted with another gas.

EMBODIMENTS OF THE INVENTION

The principle of the vapor emitting method according to the present invention allows to evaporate hydrogen peroxide vapors or mixtures with hydrogen peroxide. These vapors are subsequently used for decontamination purposes. This evaporation is achieved so, that a solution of hydrogen peroxide or mixtures thereof, are mixed with an initiator, catalyst, or catalyst source. After mixing with an initiator, catalyst, or source thereof, there occurs an initiating reaction or a catalytic decomposition, or a catalyst is formed which initiates the decomposition of peroxide. By the decomposition of peroxide, which is an exothermic reaction, and due to the stormy process of decomposition, there is evaporation of the peroxide or mixture, along with the emission of peroxide droplets or its mixtures. This process emits vapors and droplets of evaporated peroxide or mixtures, which appears under normal conditions as a smoke or steam. The resulting mixture is generated directly in the decontamination area, or is transported to the place of decontamination by pipeline. This smoke/steam contains peroxide or optionally a mixture thereof, in sufficient quantities for gaseous decontamination purposes. During the decontamination process the smoke/steam can be completely evaporated due to physical conditions, then the decontamination proceeds outside the condensation area. If there is no complete evaporation of smoke/steam due to the physical conditions, decontamination is happening in the area of condensation of used vapors. Generated vapors can be mixed with another gas for adjustment of required process parameters. The evaporation of the peroxide mixture with other substances provides greater chemical reactivity, which makes biological or chemical decontamination easier.

The vapor emitting method according to the present invention allows to generate vapors for decontamination without connecting to sources of energy and media. For the emmision of the vapors it is necessary to mix only hydrogen peroxide or mixture thereof and initiator, catalyst, or their precursor.

The subject of protection is the process of generating peroxide vapors or mixtures thereof, which replaces other methods used for gaseous decontamination purposes. The vapor emission occurs due to the catalytic or otherwise initiated decomposition of hydrogen peroxide.

EXAMPLE 1

12 ml of 69% hydrogen peroxide are metered into the vessel and the vessel is placed in the target space of 500 liters volume. 0.5 g of ferrocene is added to the surface of peroxide in the vessel. After the initial delay occurs a reaction when the ferrocene is burnt and decomposed which results in a decomposition catalyst and by higher temperature a catalytic decomposition is initiated. This reaction emits fumes of peroxide vapors that are used for decontamination.

EXAMPLE 2

To a 30 liters volume tin canister is metered 10 liters of 69% hydrogen peroxide, the vessel is placed in a target area with volume of 500 m³. 120 g of ferrocen is poured into the vessel. After the initial delay occurs the burning and decomposition of ferrocene, thereby creating a catalyst of decomposition and higher temperature starts the catalytic decomposition. This reaction emits smoke of peroxide vapors or mixtures to be used in decontamination. 

1. A method of emitting peroxide vapors or mixtures thereof, wherein the hydrogen peroxide is placed into a vessel, whereupon an initiator, catalyst or their precursor—ferrocene is added, from which the initiator or catalyst is created by reaction with peroxide or peroxide mixture.
 2. The method according to claim 1, wherein the initiator, catalyst or the precursor is selected from the group of metals such as silver, gold, platinum, palladium; metal oxides such as manganese, silver, aluminum, iron; metal salts such as manganese, aluminum, iron, silver; organometallics, manganese, iron, aluminum—e.g. ferrocene or metal-containing mixtures such as iron, aluminum, manganese, silver or the like compounds.
 3. The method according to claim 1, wherein the peroxide used is in the range of concentration between 10-90% and the temperature of usability of given configuration is from −10 to 100° C.
 4. The method according to claim 1, wherein for long-term exposure by decontaminating vapors, the process is repeated with a new charge of peroxide, or mixture and adding a new source of initiator or catalyst.
 5. The method according to claim 1, wherein the peroxide mixture is peroxide mixed with one or more substances such as peroxyacetic acid, peroxyformate acid, formic acid, boric acid, phosphoric acid, organic or inorganic carbonates, N oxides, alcohols such as tert-butyl alcohol, amines, esters; monosylic, dibasic or tribasic carboxylic acids such as oxalic acid, acetic acid, citric acid, malic acid, tartaric acid, complexing agents such as chelatones, Komlexon I, II, III, the transition metal salts catalyzing the Fenton reaction, such as salts of iron, copper, silver, manganese and zinc.
 6. The method according to claim 1, wherein the emissions of the vapor is carried out directly in the treated space, or the vapors are brought through the pipeline route to the required destination.
 7. The method according to claim 1, wherein the gases or vapors emitted are diluted with another gas. 